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THE CORPORATION OF THE TOWN OF MIDLAND

WASTEWATER OPERATIONS

2016 ANNUAL OPERATIONS REPORT

Prepared by: The Corporation of the Town of Midland Water and Wastewater Operations Department

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OVERVIEW: This annual report is prepared in accordance with the requirements of Certificate of Approval Assessment:

C OF A NUMBERS

DATE

EFFLUENT LIMITS

5708-A72SPG

JULY 20, 2016

Revokes and replaces 5708-7UZK93

8-5061-95-006

May 10, 1995

Air Approval

3-0214-80-006

March 11, 1980

Expansion of WPCP

3-0214-80-006

March 11, 1980

Air-Diesel Generator

30622-93-006

September 20, 1993

Pump Station #1

8-3288-93-006

September 24, 1993

Pump Station #1 Generator

PROJECT DESCRIPTION:

The Midland Wastewater Treatment Centre is a conventional activated sludge plant owned and operated by the Town of Midland. The facility treats a combined industrial and domestic wastewater. Treated effluent is discharged via a gravity outfall into Midland Bay. The Midland Wastewater Treatment Centre was originally built in 1965 as a primary treatment plant. In 1980 the plant was expanded adding secondary treatment. In 1995 the plant was again expanded and upgraded to the present capacity. In 2009 a standby generator was added to run the entire Wastewater Treatment Centre in the event of a power interruption. In 2016 the Certificate of Approval (C of A) was amended to include year round disinfection and de-chlorination.

PLANT FACTS:

Facilities Design Capacity – 15,665 m3 per day.

The Midland WTC consists of the following treatment units: SCADA fine screening and grit removal in headworks building primary clarification aeration secondary clarification chlorination de-chlorination sludge digestion storm equalization septage receiving

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The influent flow is measured using a partial flume in the headworks building. Effluent flow is measured based on the head behind the chlorine contact overflow weir. Phosphorus precipitation is achieved through alum addition (1,000 L/day dosage) split between the primary clarifiers and the mixed liquor flow from the final aeration basin to the secondary clarifiers. The primary underflow (sludge) is pumped to a two-stage (ESD) egg shaped anaerobic digester. Digested sludge is hauled off-site for land utilization. SCADA (Supervisory Control and Data Acquisition) The SCADA is a computerised system of monitoring the performance of the plant. It allows the operators to see changes in operating parameters as they happen instead of after it has happened. This system can also be used to control various areas of the plant and collect plant performance criteria from various instruments. Headworks The raw sewage (influent) enters the headworks via a single channel. Once in the headworks, the channel splits into two individual channels separated by a cut-water gate for a combined capacity of 2,460m3/hour. Under normal/dry weather conditions the influent flows down the primary channel, flowing through a channel monster (grinder), a self-cleaning screen and a grit removal system. In the event of a high flow exceeding 185 L/s, the cut-water gate opens automatically directing the excess flow down the secondary channel through a commutator. Leaving the headworks, flows from both the primary and secondary channels are directed to the primary clarifier influent distribution chamber. Aluminium Sulphate (coagulant) is added to these flows prior to reaching the distribution chamber for the purpose of phosphorus precipitation. Primary Clarification Three circular tanks in parallel with the capability of handling a peak flow of 32,580m3/hour are provided for primary clarification. Waste activated sludge (W.A.S.) is also added to this flow for the purpose of co-thickening the sludge in the primaries. The underflow (sludge) from each primary clarifier is then pumped on a continuous basis to the primary digester using dedicated piston pumps. The effluent from the clarifiers then enters a primary effluent collection chamber. Aeration The primary clarifier effluent proceeds directly to the aeration tanks. The aeration tank consists of six cells which can be operated in series or parallel. Currently, the plant is operating in series with six cells in service. Aeration is mechanically provided by 6 - 15 kW motors. Aluminium Sulphate (coagulant) is added to the flow (mixed liquor channel) leaving from the aeration system prior to reaching the secondary clarifiers. Secondary Clarification Flow from the aeration system proceeds to a distribution chamber feeding two circular secondary clarifiers. Sludge is removed from the bottom of each clarifier using two variable frequency drive pumps. A portion of the volume of sludge is pumped back to aeration as return activated sludge (R.A.S.) and the remainder is sent to the primary clarifiers as waste activated sludge (W.A.S.); which intern will be wasted to the primary digester.

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Chlorination From the secondary effluent collection chamber, flow proceeds directly to the chlorine contact chamber. Chlorine in the form of Sodium Hypochlorite (approximately 12%) is added year round. De-chlorination System From the Chlorine Contact Chamber, flow proceeds to the De-chlorination Chamber. Calcium Thiosulfate (captor) is added to neutralize the chlorine. Sludge Digestion The primary clarifier underflow (sludge) is directed to a two-stage anaerobic digester. The first stage consist of 1,000m3 egg shaped digester (E.S.D.) maintained at approximately 35°C using an external heat exchanger. The heat boiler is operated using digester gas supplemented with natural gas. Mixing in the first stage is accomplished by using a jet pump mixing system. The second stage consists of two conventional shaped digesters, one is fitted with a floating fibreglass cover to hold the gas produced in the system. There is a waste gas flair stack to burn off excess gas. Storm Equalization The storm equalization facility consists of a rectangular tank of approximately 1,400m3 in volume. This tank is controlled by the plant SCADA system. As the flow to the plant increases (290 L/s) in a storm event, a gate at the headworks will open and direct excess flow to this tank in order to stop plant washout in high flow (storm) situations. If the storm is of enough intensity to fill the tank, alum and chlorine are added to the tank before it overflows into a bypass chamber. This gives the storm water primary treatment before it reaches the outfall into Georgian Bay. If a by-pass does occur, the flow is also dechlorinated. Hauled Sewage Receiving The receiving station consists of 2 square tanks that the sewage haulers (holding tank and septic tank waste) can discharge into. These tanks are equipped with a mixer. As this tank is filled it can be pumped to various areas of the plant to be treated during low flow times.

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SAMPLING REQUIREMENTS: Samples of raw sewage and final effluent for the sewage treatment plant shall be collected at designated locations and analyzed for at least the following parameters at the indicated minimum frequencies:

Raw Sewage Parameter Type of Sample Minimum Frequency

BOD5 Composite weekly Total Suspended Solids Composite weekly

Total Phosphorus Composite weekly Free Ammonia Nitrogen Grab weekly Total Kjeldhal Nitrogen Composite weekly

pH Grab (on-site test) weekly

Final Effluent Parameter Type of Sample Minimum Frequency

CBOD5 Composite Weekly Total Suspended Solids Composite Weekly

Total Phosphorus Composite Weekly Total Ammonia Nitrogen Composite Weekly

E. Coli Grab Weekly Temperature Grab (on-site test) Weekly

pH Grab (on-site test) Weekly Total Chlorine Residual Grab (on-site test) Daily

The sampling and analyses required from the above conditions shall be performed in accordance with the Ministry’s Policy No. 08-06.

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Final Effluent Parameter Limits:

C. OF A. LIMITS PARAMETER CONCENTRATION LOADINGS

Annual Average CBOD5 (mg/L)

10 mg/L

Annual Average Suspended Solids

10 mg/L

T.P* Monthly Average 0.4 mg/L

Yearly Average 0.3 mg/L 1716 kg *

Monthly Average Ammonia + Am N

June 1 to August 31

10 mg/L n/a


September 1 to May 31

15 mg/L n/a

Monthly Average Total Cl Residual

0.02 mg/L n/a

Note 1: The total annual phosphorous loading is based on an annual average daily flow rate of 15,665 cubic meters per day and effluent total phosphorous concentration of 0.3 milligrams per litre. The above limits indicate the maximum concentrations and loadings that are listed in the new Certificate of Approval No. 5708-A72SPG issued July 20, 2016. SAMPLING PROCEDURES: Raw sewage samples are collected daily using an ISCO 3700 automatic sampler, composited over a 24-hour period. Once per week a 24 hr. composite sample is sent out for analysis of CBOD5, Total Suspended Solids, Total Phosphorus and TKN. Once per week a grab sample is collected and sent out for analysis of Free Ammonia Nitrogen (NH3), while daily composites collected by the ISCO 3700 are tested on site for suspended solids and soluble phosphorus. Final effluent samples are also collected daily using an ISCO 3700 automatic sampler, composited over a 24-hour period. Once per week a 24 hr. composite sample is sent out for analysis of CBOD5, Total Suspended Solids, Total Phosphorus, and Total Ammonia + Ammonium (NH3 + NH4) Nitrogen. Once per week a separate grab sample is collected and sent out for analysis of Escherichia Coli (E. Coli). Grab samples are also collected daily and

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tested on-site for pH and Total Chlorine Residual while daily composites are collected by the ISCO 3700 and tested on site for suspended solids and soluble phosphous. Raw sludge samples (grab) are collected monthly and sent out for analysis of Total Phosphorus, Total Solids, Ammonia Nitrogen, Metals, Potassium, and Ash Lol. Primary digested sludge samples (grab) are collected bi-weekly and monthly and sent out for analysis of Total Phosphorus, Total Solids, Metals, Potassium, Conductivity, Alkalinity, Volatile Acids and Ash Lol. An anaerobically digested biosolids sample (grab) is collected once per week from the second stage of the digestion process and sent out for analyses of Total Phosphorus, Total Solids, Ammonia Nitrogen, Metals and E. Coli. Currently, all samples sent out for analysis are sent to Caduceon Environmental Laboratories in the Ottawa District. On-site analysis, other than that mentioned above, is conducted for Total Phosphorus and Suspended Solids as well as other standard operating parameters. The sampling and analyses noted above are performed in accordance with the Ministry’s Policy No. 08-06. Detailed (daily) analytical data are available on request. Annual and monthly averages are summarized above. Comments: Daily Flow assessment for the 2016 year indicates that the average design capacity has not been exceeded. (Plant operating capacity is 15,665m3/day.) SLUDGE (Biosolids) MANAGEMENT: Biosolids at the plant are treated anaerobically and onsite storage capacity is limited to a maximum of 1 week. Town of Midland has an agreement with the Region of Huronia Environmental Services for the supply of all equipment and labour necessary for the transporting and disposal of Liquid Processed Organics (Biosolids) from the Town of Midland Wastewater Treatment Centre. The Contractor is responsible for the acquisition and preparation of all written materials required by the Ontario Ministry of the Environment and Climate Change (MOECC) and applications of Provincial Certificates of Approval for each Organic Soil Conditioning Site the Contractor intends to use in the execution of the contract. The Contractor is solely responsible for the operations and maintenance of the Organic Soil Conditioning sites, adhering to the Guidelines and such restrictions as maybe applied to the Provincial Certificates of Approval and any amendments that may come into effect.

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BYPASSING AND ABNORMAL CONDITIONS:

Two hypo chlorite tanks are provided, one of which is lined and heated for year round use.

The availability of the storm detention/overflow tank provides at the very least sufficient retention for primary treatment of these flows.

There is provision for chlorination and dechlorination of bypasses due to overflow of the storm equalization tank.

MAINTENANCE AND CALIBRATION ACTIVITIES: The Town of Midland Wastewater Operations plant shall maintain and operate a sufficient number of flow measuring devices, calibrated at regular intervals not exceeding one year, to ensure their accuracy to within plus or minus 5% of actual rate of flow from 10% to 100% of flow range, in order to measure:

a) The quantity of sewage being conveyed to and through the sewage treatment plant; and

b) The quantity of sewage being by-passed without complete treatment.

The waste gas burner was replaced (January 2013), meeting T.S.S.A. standards. DISCUSSION: The Midland Wastewater Treatment Centre produced excellent quality effluent in 2016. No major operational problems were encountered and the Town of Midland has met all parameters laid out in Environmental Compliance Approval with the exception of winter chlorination and de-chlorination for the month of December as approved by the Ministry of the Environment and Climate Change. We modified our chlorination and de-chlorination process by removing the existing Oxidation Reduction Potential (ORP) unit and replaced it with Wallace and Tiernan Micro 2000 Total Chlorine Analyzer (0-0.1 mg/L). This analyzer will then determine the presence of total chlorine should the proper level of de-chlorination not occur. Appendix – A. Plant Flows - 2016

B. Raw Sewage Annual Results - 2016 C. Final Effluent Annual Results - 2016 D. By-Pass Information - 2016 E. Anaerobically Digested Biosolids Summary - 2016 F. Sludge Haulage - 2016

G. Septage Received - 2016 H. RV Waste Received - 2016

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APPENDIX A

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TOWN OF MIDLAND WASTEWATER TREATMENT PLANT FLOWS

2016 AVERAGE DAILY FLOW (m3/d)

MAX. DAILY FLOW (m3/d)

MIN. DAILY FLOW (m3/d)

TOTAL FLOW (m3)

MAX. PEAK DAILY FLOW (L/s)

JANUARY 9521 14083 8197 295163 14082

FEBRUARY 10132 17709 5465 293820 17709

MARCH 12872 26080 8269 399031 26080

APRIL 12111 25136 8718 363327 25136

MAY 8134 10522 5410 252154 10522

JUNE 7254 8429 6107 217616 8429

JULY 7469 8235 6757 231542 8235

AUGUST 8273 15070 7032 256469 15070

SEPTEMBER 7609 10653 6243 228259 10653

OCTOBER 7852 10336 6654 243427 10336

NOVEMBER 7886 9868 7134 236576 9868

DECEMBER 8450 10008 7257 261952 10008

TOTAL 3279336 AVERAGE 9083.8 273278 MINIMUM 217616

MAXIMUM 399031

Notes:

Monthly Average Daily Flow - means the cumulative total sewage flow to the sewage works during a calendar month divided by the number of days during which sewage was flowing to the sewage works that month.

Maximum Daily Flow - means the maximum rate of flow to the sewage works that occurred on one given day that month.

Minimum Daily Flow - means the minimum rate of flow to the sewage works that occurred that month.

Total Flow - means the total sewage flow to the sewage works that occurred during a calendar month.

Maximum Peak Flow - means the maximum rate of sewage flow to the sewage works which occurred at a specific moment in time.

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APPENDIX B

TOWN OF MIDLAND WASTEWATER TREATMENT PLANT RAW SEWAGE MONTHLY CONCENTRATIONS

YEAR RAW

INFLUENT BOD5

(mg/L)

RAW INFLUENT

T.P. (mg/L)

RAW INFLUENT

S.S. (mg/L)

RAW INFLUENT

T.K.N. (mg/L)

UN-IONIZED

AMMONIA (mg/L)

RAW INFLUENT pH (mg/L)2016

JANUARY 100 3.0 166 21.45 0.68 7.6

FEBRUARY 138 2.8 164 23.08 0.32 7.5

MARCH 85 3.2 137 16.48 0.18 7.5

APRIL 90 3.0 148 22.03 0.28 7.6

MAY 189 3.5 213 25.94 1.02 8.0

JUNE 166 4.0 271 29.06 4.84 8.1

JULY 153 3.7 181 28.18 1.51 7.9

AUGUST 131 3.8 188 25.48 1.36 8.1

SEPTEMBER 136 3.7 189 25.60 3.27 8.2

OCTOBER 163 4.1 190 30.50 2.57 8.3

NOVEMBER 149 4.2 213 36.08 1.95 8.2

DECEMBER 134 3.5 194 26.33 1.53 8.1

YEARLY AVG. 136 3.54 187.67 25.84 1.67 7.9

Notes:

Monthly Average Concentration - means the arithmetic mean of all daily or weekly concentrations of a contaminant in the raw influent sampled or measured, during a calendar month.

Raw Influent - means raw (untreated) wastewater flowing into the treatment plant.

BOD5 - means five day biochemical oxygen demand measured in an unfiltered sample.

Raw Influent T.P. - means the total phosphorus concentration.

Raw Influent S.S. - refers to the concentration of solids that either float on the surface or are suspended in the raw wastewater entering the sewage works.

Raw Influent T.K.N. - refers to the concentration of total Kjeldahl nitrogen in the raw influent sample.

Raw Influent T.A.N. - refers to the concentration of total ammonia and ammonium nitrogen in the raw influent sample.

Un-ionized ammonia - also called free ammonia, refers to the neutral form of ammonia-nitrogen in water.

Raw Influent pH - refers to the intensity of the basic or acidic condition of a liquid; measures the hydrogen ion concentration.

APPENDIX C

TOWN OF MIDLAND WASTEWATER TREATMENT PLANT FINAL EFFLUENT MONTHLY CONCENTRATIONS

YEAR FINAL EFF.

CBOD5

(mg/L)

FINAL EFF. T.P.

(mg/L)

FINAL EFF. S.S.

(mg/L)

FINAL EFF.

T.A.N. (mg/L)

FINAL EFF. Ph (mg/L)

FINAL EFF. E. coli

(org/100mL)

FINAL EFF. TOT.

NAOCl RES.

(mg/L) CONDUCTIVIT

Y (mg/L)

AVG. O.R.P

READING (mV)

MAX. O.R.P.

READING (mV)

MIN. O.R.P.

READING (mV) 2016

JANUARY 6.0 0.15 3.9 0.205 7.2 743.5 940.2

FEBRUARY 8.0 0.12 3.5 3.54 7.2 1037.7 937.8

MARCH 5.3 0.16 4.0 1.04 7.1 441.6 906.8

APRIL 3.0 0.12 2.5 1.58 7.1 220.4 838.5

MAY 3.4 0.11 3.4 6.17 7.5 44.5 0.54 942.9 123.7 1000.0 0

JUNE 3.0 0.14 3.3 0.106 7.5 21.7 0.58 1033.7 74.2 1000.0 0

JULY 3.0 0.13 2.0 0.07 7.4 26.0 0.63 1046.6 141.6 241.2 0

AUGUST 3.8 0.18 2.4 0.21 7.5 6.3 0.65 1041.0 122.3 1000.0 0

SEPTEMBER 3.0 0.09 1.8 0.067 7.6 9.2 0.6 1036.0 130.6 200.9 0

OCTOBER 3.0 0.08 2.4 0.11 7.6 13.63 0.58 951.8 119.42 159.2 0

NOVEMBER 3.8 0.11 2.6 0.056 7.4 19.7 0.58 967.1 134.7 1000.0 0

DECEMBER 3.0 0.15 4.7 4.825 7.4 1012.9 *0.019 905.8 OFF LINE OFF LINE OFF LINE

TOTAL

AVERAGE 4.0 0.13 3.0 1.59 7.4 299.8 0.59 962.35 120.9 ANNUAL

AVG.

426.31

LOADING (Kg/Yr.)

*CHLORINATED 2 DAYS IN DECEMBER.

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Notes:

Monthly Average Concentration - means the arithmetic mean of all daily or weekly concentrations of a contaminant in the final effluent sampled or measured during a calendar month.

Final Effluent - refers to the treated wastewater discharging from the treatment plant.

CBOD5 - means five day biochemical oxygen demand measured in an unfiltered sample. Both the BOD and COD tests are a measure of the relative oxygen-depletion effect of a waste contaminant.

Final Effluent T.P. - means the total phosphorus concentration in a given sample.

Final Effluent S.S. - refers to the concentration of solids that either float on the surface or are suspended in the final effluent discharging the wastewater plant.

Final Effluent T.A.N. - refers to the concentration of total ammonia and ammonium nitrogen in the final effluent sample.

Final Effluent pH - refers to the intensity of the basic or acidic condition of a liquid; measures the hydrogen ion concentration.

Final Effluent E. Coli - Escherichia coli, indicator organisms to test environmental samples for fecal contamination.

Final Effluent Total NaOCl Residual - refers to the remaining concentrations of oxidizing hypochlorous acid and hypochlorite ions to estimate effectiveness of disinfection or to demonstrate safety for discharge to aquatic ecosystems.

O.R.P. Reading - Oxidation reduction potential is a measure of the tendency of a chemical species to acquire electrons and thereby be reduced. Reduction potential is measured in millivolts (mV). It is used as an indicator of dechlorination.

Monthly Average O.R.P. Reading - means the arithmetic mean of all daily measured readings in the final effluent sample during a calendar month.

Maximum O.R.P. Reading - refers to the maximum measured value in a given calendar month.

Minimum O.R.P. Reading - refers to the minimum measured value in a given calendar month.

Final Effluent Parameter Limits:

C. OF A. LIMITS PARAMETER CONCENTRATION LOADINGS

Annual Average CBOD5 (mg/L)

10 mg/L

Annual Average Suspended Solids

10 mg/L

T.P* Monthly Average 0.4 mg/L

Yearly Average 0.3 mg/L 1716 kg*


June 1 to August 31

10 mg/L n/a


September 1 to May 31

15 mg/L n/a

Monthly Average Total Cl Residual

0.02 mg/L n/a

Notes: *Note 1: The total annual phosphorous loading is based on an annual average daily flow rate of 15,665 cubic meters per day and effluent total phosphorous concentration of 0.3 milligrams per litre.

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APPENDIX D

BY-PASS REPORT - 2016

Month Location Type Volume

(m3) Duration

(min) # Events Rainfall

(mm) January February

March 28 Storm Tank Plant

Bypass 4082.2 12 hours 3 44.5

March 31 Storm Tank Plant

Bypass 4729.9 14.43 hrs 6 54.0

March 31 Chamber A Plant

Bypass 24.5 0.23 hr 1 54.0 April May

June

July 8 Chamber A Plant

Bypass 25.0 0.3 hr 1 21.5

August 16 Storm Tank Plant

Bypass 645.8 1.7 hr 2 73.0

Chamber A Plant

Bypass 28.4 0.17 hr 2 73.0 September

17 Chamber A Plant

Bypass 43.0 .25 hr 1 45.0

October 17 Chamber A Plant

Bypass 116.5 0.3 hr 1 39.0 November December

NOTES:

Plant By-pass - means any discharge from a pump station or chamber that does not undergo any treatment before it was discharged to the environment.

Secondary By-pass - means any discharge from within the wastewater treatment plant that received partial treatment before it was discharged to the environment.

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APPENDIX E

DIGESTED BIOSOLIDS PARAMETER LIMITS:

PARAMETER CONCENTRATION Antimony 1 ug/g Arsenic 11 ug/g Barium 210 ug/g

Beryllium 2.5 ug/g Boron 36 ug/g

Boron (HWS) NA Cadmium 1 ug/g Chromium 67 ug/g

Chromium (VI) 0.66 ug/g Cobalt 19 ug/g Copper 62 ug/g

Lead 45 ug/g Mercury 0.16 ug/g

Molybdenum 2 ug/g Nickel 37 ug/g

Selenium 1.2 ug/g Silver 0.5 ug/g

Thallium 1 ug/g Uranium 1.9 ug/g

Vanadium 86 ug/g Zinc 290 ug/g

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APPENDIX F

2016 HAULED BIOSOLIDS

DATE: NUMBER OF LOADS

VOLUME HAULED M3

JANUARY 26 1,092

FEBRUARY 32 1,344

MARCH 19 798

APRIL 23 966

MAY 30 1,260

JUNE 26 1,092

JULY 22 924

AUGUST 25 1,048

SEPTEMBER 30 1,261

OCTOBER 26 1,095

NOVEMBER 23 966

DECEMBER 31 1,280

TOTAL 313 13,126

APPENDIX G

TOWN OF MIDLAND WATER & WASTEWATER OPERATIONS MONTHLY UPDATED TOTAL

HAULED SEWAGE DISPOSAL BREAKDOWN ‐ 2016 570700

GEORGIAN BAY SANITATION

DOMESTIC DOMESTIC COM./IND. COM/IND. PORTABLE MARINE GREASE HAULED FROM SEPTIC HOLDING SEPTIC HOLDING TOILETS WASTE TRAPS MUNICIPALITY

MONTH TANK TANK TANK TANK # OF TIMES

JANUARY 1000 27200 2000 1000 TINY 82 FEBRUARY 24200 TAY 20

MARCH 1600 24600 2000 PENETANG 12 APRIL 1000 53400 1000 CRAIGHURST

MAY 6600 12000 1000 2000 SPRINGWATER 1 JUNE 8000 5000 9000 4000 ORR LAKE JULY 800 10600 8000 9000 7000 OTHER 3

AUGUST 13800 2000 5000 7000 13000 MIDLAND 49

SEPTEMBER 9200 4000 5600 2000 TOTAL 167

OCTOBER 12000 3000 2000 NOVEMBER 4000 22700 4000 4000 2000 DECEMBER 800 18200 1000

TOTALS: 9200 230500 2000 40000 43600 32000 0

HAULED SEWAGE TOTAL IN GALLONS 357300

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TOWN OF MIDLAND WATER & WASTEWATER OPERATIONS HAULED SEWAGE DISPOSAL BREAKDOWN ‐ 2016

REGIONAL SANITATION



JANUARY 20000 TINY 40 FEBRUARY 18000 TAY 5

MARCH 27000 PENETANG 12 APRIL 8000 CRAIGHURST MAY 3000 SPRINGWATER JUNE 9000 ORR LAKE JULY 18000 OTHER

AUGUST 15000 MIDLAND 2

SEPTEMBER 17000 TOTAL 59

OCTOBER 6000 NOVEMBER 5500 3000 DECEMBER 9600

TOTALS: 0 91100 0 0 0 68000 0


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TOWN OF MIDLAND WATER & WASTEWATER OPERATIONS HAULED SEWAGE DISPOSAL BREAKDOWN ‐ 2016

RITCHIE SEPTIC TANK PUMPING



JANUARY 3800 TINY 3 FEBRUARY 7000 2000 TAY 2

MARCH 7500 7000 PENETANG APRIL 6000 2000 ELMVALE/SW 12 MAY COLDWATER JUNE ORR LAKE 2 JULY OTHER

AUGUST MIDLAND

SEPTEMBER TOTAL 19

OCTOBER NOVEMBER DECEMBER

TOTALS: 0 24300 0 11000 0 0 0


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TOWN OF MIDLAND WATER & WASTEWATER OPERATIONS

HAULED SEWAGE DISPOSAL BREAKDOWN ‐ 2016

PEPI SEWAGE DISPOSAL



JANUARY 2600 TINY FEBRUARY 3400 2000 TAY 5

MARCH 5000 2000 HONEY

HARBOUR APRIL 2000 MUSKOKA MAY SEVERN TOWN 4 JUNE COLDWATER JULY G‐BAY 2

AUGUST MIDLAND

SEPTEMBER TOTAL 11

OCTOBER NOVEMBER DECEMBER 2000

TOTALS: 0 13000 0 6000 0 0 0


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DS DH CII‐S CII‐H PT MW GT YR END TOTALS

Gallon Total 9200 358900 2000 57000 43600 100000 0 570700

m3 41.86 1632.995 9.1 259.35 198.38 455 0 2596.685

% 1.6 62.9 0.4 10.0 7.6 17.5 0.0 100.0

MUNICIPALITIES TOTAL 256

APPENDIX H

DISPOSAL B Municipality VOLUMETOWN in gallons

13-Apr-16 MIDLAND 20

9-May-16 PENETANG 15

27-May-16 MIDLAND 10

6-Jun-16 MIDLAND 10

8-Jun-16 MIDLAND 10

10-Jun-16 MIDLAND 5

13-Jun-16 MIDLAND 40

17-Jun-16 PENETANG 10



23-Jun-16 WYEBRIDGE 10


7-Jul-16 TINY 10

25-Jul-16 MIDLAND 5

25-Jul-16 MIDLAND 5

25-Jul-16 MIDLAND 5

26-Jul-16 PENETANG 5

2-Aug-16 WAUBAUSHENE 5

3-Aug-16 MIDLAND 10

4-Aug-16 TINY 5

9-Aug-16 MIDLAND 5

11-Aug-16 PENETANG 60

18-Aug-16 WYEBRIDGE 5

19-Aug-16 WAUBAUSHENE 10

29-Aug-16 ALABAMA 20

30-Aug-16 MIDLAND 50

30-Aug-16 SPRINGWATER 20

6-Sep-16 MIDLAND 35

8-Sep-16 TAY 20

13-Sep-16 QUEENS 10

DISPOSAL B MIDLAND 35

22-Sep-16 WAUBAUSHENE 20

27-Sep-16 PENETANG 80

27-Sep-16 TAY 20

29-Sep-16 PENETANG 20

13-Oct-16 MIDLAND 10

14-Oct-16 BARRIE 10

14-Oct-16 WAUBAUSHENE 10


18-Oct-16 SEVERN SOUND 10


18-Oct-16 PENETANG 5





28-Oct-16 TINY 5

1-Nov-16 TINY 10

2-Nov-16 MIDLAND 10

2-Nov-16 MIDLAND 20

2-Nov-16 MIDLAND 30

4-Oct-16 TINY 20

16-Oct-16 WAUBAUSHENE 20

14-Nov-16 MIDLAND 20

14-Nov-16 PORT SEVERN 20

Total 915

RV Waste Disposal 2016

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